Centrifugal combustion method using air-flow in a furnace

ABSTRACT

This invention, Centrifugal and Divided Space combustion method, need to install a cylindrical fuel pot, the first combustion chamber, the second combustion chamber and an exhaust pot. It also needs to install the upper and the lower pots outside the first combustion chamber and the fuel pot in order to have the lower and the upper air paths inside the outer pots. One or several ventilator(s) to make air-flow is tangentially connected to the upper and the lower air paths at the lower part of the upper outer pot. And several air-flow control devices should be located at the upper part of the upper air path. Thus, the invention is composed to realize the complete combustion only with the air supply into the furnace. In this case, the space in the furnace is divided into many combustive sectors by the air-flow.

TECHNICAL FIELD

[0001] The present invention relates, in general, to a centrifugal combustion method using air-flow in a furnace and, in particular, to a centrifugal combustion method using air-flow in a furnace, in which combustibles such as low-calorie wastes with high moisture content, high-calorie plastics and rubbers with low moisture content, and high-calorie waste liquid are completely and rapidly combusted at high temperature by only supplying air into the furnace without auxiliary devices and fuel while a space in the furnace is divided into many combustive sectors by air-flows due to a centrifugal force of air under high pressure rapidly supplied to the furnace and revolved in high speed in the furnace.

BACKGROUND ART

[0002] A conventional method for combusting wastes or waste oil, comprises the steps of supplying combustibles into a combustion chamber in a furnace; igniting combustibles in the combustion chamber with the use of an ignition burner; combusting combustibles with cool air directly supplied to an upper, a mid, and a lower part of the combustion chamber.

[0003] However, the conventional method has disadvantages in that high-calorie, low-calorie, and wet wastes are incompletely combusted, and combustion efficiency is low because wastes are combusted with only cool air supplied through a ventilator. Incompletely combusted combustibles remain or end up in a landfill, and so resources are wasted and an environment is polluted. In addition, incomplete combustion of combustibles causes various toxic substances fatal to humans, such as dioxin as well as carbon dust to be emitted into the atmosphere, and the burner is continuously operated and auxiliary fuel (e.g. diesel fuel) is additionally used because incompletely combusted remains should be again combusted, thereby the cost of fuel is high, combustion time is long, and combustion efficiency is lowered.

[0004] Furthermore, other disadvantages of the conventional method are that a special burner capable of being used at high temperatures is needed, air is supplied to the furnace under high pressure, and refractory bricks should be constructed inside of the furnace because combustibles are combusted at high temperature, and so combustion cost becomes high. Particularly, a combustion chamber made of metals does not endure high temperatures and thus the chamber is eroded, thereby durability of the furnace is reduced.

DISCLOSURE OF THE INVENTION

[0005] Accordingly, the present invention has been made keeping in mind the above problems occurring in the prior art, and an object of the present invention is to provide a centrifugal combustion method in which combustibles are completely combusted at 1500 to 1900° C. by air circulation without any additional device or catalyst.

[0006] Another object of the present invention is to provide a centrifugal combustion method, in which low-calorie fuel is sufficiently combusted without auxiliary fuel and about 100% of heat produced during combustion of the low-calorie fuel is utilized.

[0007] It is still another object of the present invention to provide a centrifugal combustion method, in which high-calorie fuel is sufficiently combusted without auxiliary fuel and about 100% of heat produced during combustion of the high-calorie fuel is utilized.

[0008] It is yet another object of the present invention to provide a centrifugal combustion method, in which wet fuel or waste containing a humidity of 100% or less is sufficiently combusted without auxiliary fuel and heat produced during combustion of the wet fuel or waste containing a humidity of 100% or less is sufficiently utilized.

[0009] It is a further object of the present invention to provide a centrifugal combustion method, in which combustibles are completely combusted in the same size combustion chamber as a conventional furnace (incinerator) at a speed several times quicker than a conventional combustion method.

[0010] Based on the present invention, the above objects can be accomplished by provision of a furnace comprising a cylindrical fuel tank; a cylindrical first combustion chamber; a cylindrical second combustion chamber; a cylindrical exhaust tub; an upper and a lower outer tub wrapping the first combustion chamber and the fuel tank such that spaces are formed between the upper outer tub and the first combustion chamber, and between the lower outer tub and the fuel tank; one or several ventilator(s) connected to a lower part of the upper outer tub such that the ventilator is tangentially communicated with a space between, the first combustion chamber and the upper outer tub, and to an upper part of the lower outer tub through air connection pipe(s) such that the ventilator is tangentially communicated with a space between the fuel tank and the lower outer tub; a plurality of air-flow control devices positioned at an upper part of the space between the first combustion chamber and the upper outer tub.

[0011] In the furnace, combustibles are completely and rapidly combusted at high temperature while a space in the furnace is divided into many combustive sectors by air-flows owing to a centrifugal force of air under high pressure rapidly supplied to the furnace and revolved at high speed in the furnace.

BRIEF DESCRIPTION OF THE DRAWINGS

[0012] The above and other objects, features and other advantages of the present invention will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawings, in which:

[0013]FIG. 1 is a longitudinal sectional view of a furnace according to the present invention, with an air-flow inside of the furnace being shown;

[0014]FIG. 2a is a transverse sectional view of the furnace taken along the line A-A of FIG. 1, with the air-flow inside of the furnace being shown;

[0015]FIG. 2b is a transverse sectional view of the furnace taken along the line B-B of FIG. 1, with the air-flow inside of the furnace being shown;

[0016]FIG. 2c is a transverse sectional view of the furnace taken along the line C-C of FIG. 1, with the air-flow inside of the furnace being shown;

[0017]FIG. 2d is a transverse sectional view of the furnace taken along the line D-D of FIG. 1, with the air-flow inside of the furnace being shown;

[0018]FIG. 3 is a longitudinal sectional view of the furnace according to the present invention, with a plurality of combustive -sectors divided by the air-flow being shown;

[0019]FIG. 4a is a longitudinal sectional view of the furnace with the pre-heated air-flow in a and g parts of the furnace being shown;

[0020]FIG. 4b is a longitudinal sectional view of a portion of the furnace with the pre-heated air-flow in b part of the furnace being shown;

[0021]FIG. 4c is a longitudinal sectional view of a portion of the furnace with an exhaust air-flow in c and f parts of the furnace being shown;

[0022]FIG. 4d is a longitudinal sectional view of a portion of the furnace with the exhaust air-flow in d part of the furnace being shown; and

[0023]FIG. 4e is a longitudinal sectional view of a portion of the furnace with the exhaust air-flow in e part of the furnace being shown.

BEST MODE FOR CARRYING OUT THE INVENTION

[0024] Reference should now be made to the drawings, in which the same reference numerals are used throughout the different drawings to designate the same components.

[0025] In order to accomplish a centrifugal combustion method according to the present invention, provided is a furnace 50, comprising a flange 2 positioned around a lower part of a cylindrical first combustion chamber 1 and outwardly protruded from the first combustion chamber 1; an upper and a lower outer tub 3 and 4 firmly set over and under the flange 2, respectively; a fuel tank 6 positioned under the first combustion chamber 1, while an upper side of the fuel tank 6 being opened and in close contact with a bottom of the flange 2 of the first combustion chamber 1, and a lower side of the fuel tank 6 being combined with a hydraulic jack 5 for attaching/detaching the fuel tank 6; a flange 9 outwardly protruded from a lower part of a second combustion chamber 8 having an exhaust tub 7 positioned on an upper side thereof, and positioned on an upper part of the upper outer tub 3; one or plural ventilator(s) 11 connected to an air supply pipe 10 which is tangentially connected to the lower part of the upper outer tub 3, and connected through an air connection pipe 13 to an air suction pipe 12 which is connected to the upper part of the lower outer tub 4 such that the ventilator 11 is communicated with the air suction pipe 12; an air direction control plate 14 positioned on an upper part of a space between the first combustion chamber 1 and the upper outer tub 3, and positioned at the upper part. of the upper outer tub 3; and a plurality of air-flow control devices 16 positioned at the upper part of the upper outer tub 3, and each consisting of an air direction control plate 14 and a control rod 15 rotatably combined with the air direction control plate.

[0026] In addition, the furnace 50 according to the present invention comprises an opening/shutting door positioned at the lower outer tub 4 covering the fuel tank 6, through which entrance and exit of the fuel tank 6 is allowed, and a plurality of rollers firmly set on a bottom of the fuel tank 6 for transporting the fuel tank 6 by use of rails, even though the opening/shutting door and rollers are not shown in drawings.

[0027] According to the present invention, a centrifugal combustion method using air-flow in a furnace, comprises the steps of firstly preheating cool air by absorbing a caloric heat from an exterior wall of a fuel tank 6, in which ventilator noise is reduced by sucking the cool air through a space between the fuel tank 6 and a lower outer tub 4 with the use of the ventilator 11; supplying the firstly preheated air to a ventilator and secondly preheating the firstly preheated air supplied into a space between a first combustion chamber 1 and an upper outer tub 3, in which the firstly preheated air absorbs a caloric heat of the first combustion chamber 1 and simultaneously cools the exterior wall of the first combustion chamber 1 while ascending and revolving at high speed; controlling the amount of the secondly preheated air, which ceases to ascend because a flange 9, positioned at a lower part of the second combustion chamber 8, obstructs ascending of the secondly preheated air in the first combustion chamber 1 and the second combustion chamber 8 by controlling an angle of an air-flow control device 16; thirdly preheating the secondly preheated air fed to the first combustion chamber, in which secondly preheated air revolving in contact with an interior wall of the first combustion chamber due to a centrifugal force produced by the secondly preheated air continuously revolving in the first combustion chamber, and descending into the fuel tank while absorbing caloric heat from the interior wall of the first combustion chamber and simultaneously cooling the interior walls of the first combustion chamber 1 and the fuel tank 6; forming a mixed ignition combustive sector f, in which the thirdly preheated air-flow b is mixed with fuel in the fuel tank 6, and the resulting mixture revolves and is combusted; forming a high gravity combustive sector c, in which high gravity combustibles incompletely combusted in the mixed ignition combustive sector f are fed into the thirdly preheated air b in the first combustion chamber 1 while being combusted in a sufficiently long combustion distance and a lengthy period of combustion time; forming a low gravity high temperature combustive sector d, in which low gravity combustibles incompletely combusted in the high gravity combustive sector c are transferred into a center of the first combustion chamber 1, collected, and ascend while revolving and being combusted; forming a high temperature heat core sector e, a temperature of which is maximum in the furnace, at a center of the furnace; completely combusting combustibles not thermally decomposed in the low gravity high temperature combustive sector d and the high temperature heat core sector 2 nor emitted, in which the combustibles descend due to gravity of the combustible and are transferred into a thirdly preheated air-flow b to be re-combusted; completely combusting remains incompletely combusted in the first combustion chamber 1 in conjunction with the secondly preheated high temperature air a ascending through the air-flow control device 16 in the second combustion chamber 8 and simultaneously cooling the interior wall of the second combustion chamber 8; and emitting combustion gas through an exhaust tub 7.

[0028] The furnace 50 is operated, as follows.

[0029] After fuel 17 filled in the fuel tank 6 is ignited by a hand or automatic ignition device, an upper side of the fuel tank 6 is closely attached to a bottom of the flange 2 positioned at a lower part of the first combustion chamber 1 through a hydraulic jack 5 for attaching/detaching the fuel tank 6. Next, a caloric heat is produced during mixing of fuel with air and combusting of the resulting mixture in the fuel tank 6, and the exterior wall of the fuel tank 6 is cooled and cool air 5 supplied through a bottom of the lower outer tub 4 is firstly preheated while the cool air flows through a space between the fuel tank 6 and the lower outer tub 4, by operating the ventilator 11 at high speed. The firstly preheated air g is tangentially supplied through the ventilator 11 into a space between the first combustion chamber 1 and the upper outer tub 3 and ascends by revolving at high speed. At this time, firstly preheated air g supplied by the ventilator 11 absorbs the caloric heat of the first combustion chamber 1 to be changed into a secondly preheated high temperature air a, as well as cools an exterior wall of the first combustion chamber 1. When air ascending by revolving in a space between the first combustion chamber 1 and the upper outer tub 3 reaches a bottom of the flange 9 of the second combustion chamber 8, the air does not ascend any more because the flange 9 obstructs ascending of the air, and the amount of air supplied into the first combustion chamber 1 and the second combustion chamber 8 can be controlled by an angle of an air direction control plate 14, which is positioned under the flange 9 of the second combustion chamber 8, changed with rotation of control rods 15 of air-flow control devices 16.

[0030] Because polymer based high-calorie wastes such as waste vinyl, waste plastic, and waste tires have many volatile components and rapidly decompose, when the polymer based high-calorie wastes are in contact with high temperature air, a temperature of combustibles is increased and thus sooty smoke is produced due to an incomplete combustion, in conjunction with an explosive combustion.. At this time, if the air direction control plate 14 of the air-flow control device 16 is at an angle of 135° with a revolution direction of air (as shown in drawings), the amount of secondly preheated high temperature air a descending to the first combustion chamber 1 is reduced and a combustion rate becomes slow, thereby preventing the explosive combustion. In addition, substances incompletely combusted in the first combustion chamber 1 are completely combusted with secondly preheated sufficiently high temperature air by increasing the amount of air supplied into the second combustion chamber 8.

[0031] On the other hand, when the air direction control plate 14 of the air-flow control device 16 is at an angle of 45° with a revolution direction of air, the amount of air supplied to the, first combustion chamber 1 is increased and the amount of air supplied to the second combustion chamber 8 is decreased. In other words, a combustion rate, a combustion temperature, and a required heat capacity per hour can be controlled by the air-flow control device 16.

[0032] Air supplied to the first combustion chamber 1 is not diffused to a center of the first combustion chamber 1 because of the centrifugal force which is due to a continuous revolution of air, but descends into the fuel tank 6 storing fuel 17 while revolving in close contact with the interior wall of the first combustion chamber 1. At this time, the air supplied to the first combustion chamber 1 cools the interior wall of the first combustion chamber 1, which is heated by radiation heat from the high gravity combustive sector c, the low gravity high temperature combustive sector d, and the high temperature heat core sector in the first combustion chamber 1, and is simultaneously changed into the thirdly preheated high temperature air b.

[0033] Thirdly preheated high temperature air b supplied to the fuel tank 6 is revolved at high speed and mixed with fuel 17, the resulting mixture is then combusted in the mixed ignition combustive sector f before it is transferred to a center of the first combustion chamber 1. At this time, high temperature atoms or molecules are transferred to the low gravity high temperature combustive sector d and high temperature heat core sector 2 which is a maximum temperature in the first combustion chamber 1, and ascend while revolving in high temperature and high speed, thereby the mixture of the thirdly preheated air b with fuel 17 is completely combusted.

[0034] Additionally, high gravity combustibles are transferred to the high gravity combustible sector c closer to the center of the first combustion chamber 1 than thirdly preheated air-flow b, revolves in high speed at high temperature, and are combusted while securing a sufficiently long combustion distance and time. Combusted combustibles become greatly reduced in gravity to the extent of approaching zero, and are transferred to the low gravity high temperature combustive sector d and the high temperature heat core sector e to be completely combusted at high speed and at high temperature.

[0035] Meanwhile, combustibles not thermally decomposed in the low gravity high temperature combustive sector d and the high temperature heat core sector e. descend due to the weight of the combustible, and are transferred to the thirdly preheated air-flows b and again combusted, thereby the combustible is completely combusted.

[0036] Remains incompletely combusted in the first combustion chamber 1 are completely combusted with secondly preheated high temperature air-flow a ascending through the air-flow control device 16 in the second combustion. chamber 8, which simultaneously cools the interior wall of the second combustion chamber 8, thus nonpolluting combustion gas is emitted through an exhaust tub 7.

[0037] Furthermore, because the lower outer tub 4 is positioned outside of the fuel tank 6 in such a way that a space is formed between the fuel tank 6 and the lower outer tub 4, cool air sucked by the ventilator 11 and passing through the space between the fuel tank 6 and the lower outer tub 4 cools the exterior wall of the fuel tank 6, and simultaneously absorbs the caloric heat of the fuel tank 6 to be preheated. In addition, because the space between the fuel tank 6 and the lower outer tub 4 acts as a suction path, and the cool air passing through the space is firstly preheated before being supplied into the ventilator 11, noise from the ventilator 11 is reduced, in comparison with the conventional ventilator which sucks cool air directly from the atmosphere.

[0038] After polymer based high-calorie wastes such as waste vinyl, waste plastic, waste tires, and waste oil was incinerated according to the centrifugal combustion method of the present invention, a temperature distribution in the furnace 50 was measured to be 100 to 200° C. in the secondly preheated air a, 300 to 500° C. in the thirdly preheated air b, 1000 to 1200° C. in the mixed ignition combustive sector f, 1200 to 1400° C. in the high gravity combustive sector c, 1300 to 1500° C. in the low gravity high temperature combustive sector d, and 1500 to 1900° C. in the high temperature heat core sector e.

[0039] Therefore, the present invention provides a centrifugal combustion method, characterized in that toxic substances fatal to humans such as dioxins are completely decomposed at high temperature and only nonpolluting gas is emitted to the atmosphere because only combustion gas of 1300° C. or higher thermally decomposed in the low gravity high temperature combustive sector d and the high temperature heat core sector e is emitted.

INDUSTRIAL APPLICABILITY

[0040] As described above, the present invention provides a centrifugal combustion method, in which combustibles can be completely combusted at high temperature by supplying air through a ventilator into a furnace without any separate auxiliary device or auxiliary fuel and by dividing a space in the furnace into many combustive sectors with the use of a centrifugal force due to high speed revolution of air. The centrifugal combustion method of the present invention has advantages in that although materials of the furnace are not special refractory materials but metals, the furnace can be durably used without a conventional special burner capable of enduring high speed and temperature combustion, supplying of oxygen under high pressure, and a firebrick used to protect the wall of the furnace because a caloric heat is absorbed by preheated air-flow revolving in high speed around an interior and an exterior wall of a first combustion chamber, and around interior walls of a fuel tank and a second combustion chamber and thus excessive of heating of the fuel, the first and the second combustion chamber, and the upper and the lower outer tub are prevented.

[0041] Other advantages of the present invention are that size and weight of the furnace according to the present invention are reduced by two times or more in comparison with a conventional furnace because a structure is simple and a high temperature and high speed combustion is realized, inflammable substances not usually suitable for incineration can be rapidly incinerated, a boiler used in a vinyl house or bathhouse reutilizes a complete combustion heat in order to save energy, and construction and operational costs of a sanitary landfill are saved because completely combusted gas is emitted from the incineration furnace in order to avoid polluting an environment.

[0042] The present invention has been described in an illustrative manner, and it is to be understood that the terminology used is intended to be in the nature of description rather than of limitation. Many modifications and variations of the present invention are possible in light of the above teachings. Therefore, it is to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described. 

1. A centrifugal combustion method using air-flow in a furnace, comprising the steps of: firstly preheating cool air supplied from a lower part of a lower outer tub through a space between a fuel tank and the lower outer tub; supplying the firstly preheated air to a ventilator and secondly preheating the firstly preheated air in a space between a first combustion chamber and an upper outer tub; thirdly preheating the secondly preheated air fed to the first combustion chamber, said secondly preheated air revolving in contact with an interior wall of the first combustion chamber due to a centrifugal force produced by the secondly preheated air continuously revolving in the first combustion chamber, and descending into the fuel tank while absorbing caloric heat from the interior wall of the first combustion chamber; forming a mixed ignition combustive sector, in which the thirdly preheated air is mixed with fuel in the fuel tank, and a resulting mixture revolves and is combusted; forming a high gravity combustive sector, in which high gravity combustibles incompletely combusted in the mixed ignition combustive sector are fed into the thirdly preheated air in the first combustion chamber while being combusted in a sufficiently long combustion distance and a lengthy period of combustion time; forming a low gravity high temperature combustive sector, in which low gravity combustibles incompletely combusted in the high gravity combustive sector are transferred into a center of the first combustion chamber, collected, and ascend while revolving and being combusted; and forming a high temperature heat core sector at a center of the furnace.
 2. The method according to claim 1, wherein noise of the ventilator is reduced by sucking the cool air from the lower part of the lower outer tub through the space between the fuel tank and the lower outer tub into the ventilator.
 3. The method according to claim 1, wherein a plurality of air-flow control devices are located at an upper part of the upper outer tub, and control a combustion rate, a combustion temperature, and a required heat capacity per hour, said air-flow control devices each consisting of an air direction control plate positioned at an upper part of the space between the first combustion chamber and the upper outer tub, and a control rod rotatably combined with the air direction control plate.
 4. The method according to claim 1, wherein the fuel tank, an interior and an exterior wall of the first combustion chamber, and an interior wall of the second combustion chamber are protected from combustion heat by the firstly, secondly, and thirdly preheated air-flows. 